Electrochemical cell cathode material

ABSTRACT

There is provided a primary cell having an anode material, an electrolyte material and a cathode material, wherein the cathode material, in the pre-discharge condition thereof, is Na 6  V 10  O 28 . In one aspect, the invention comprises a thermal cell having a lithium metal or lithium alloy anode, an electrolyte material comprising at least one lithium salt and the aforementioned cathode material. In another aspect, the invention comprises an improved conventional room or ambient temperature cell having a lithium anode, a nonaqueous electrolyte and the aforementioned cathode material.

RIGHTS OF THE GOVERNMENT

The invention described herein may be manufactured and used by or for the Government of the United States for all governmental purposes without the payment of any royalty.

BACKGROUND OF THE INVENTION

The present invention relates to electrochemical cells and primarily to cells having a lithium metal or lithium alloy anode.

Thermal cells are primary electrochemical cells having an anode, a cathode and an electrolyte that is solid and non-conductive at ambient temperatures. The cell is activated by providing sufficient heat to melt the electrolyte which thereby becomes conductive. Thermal batteries are made up of a plurality of thermal cells. These batteries conventionally include a heat source, generally an ignitable, exothermically reactive chemical charge or pyrotechnic.

Thermal batteries are normally used to generate a single continuous energy output, once activated. The duration of the output may vary from a few seconds to an hour, depending on the battery design and construction. These batteries are frequently used as power sources for guided missiles and other weapons systems.

A variety of electrochemical systems are known for use in thermal cells. Known anode materials include the alkali metals and their alloys, alkaline earth metals and their alloys and aluminum. The electrolytes are generally mixtures of alkali metal halides, commonly a eutectic mixture of LiCl and KCI melting at about 352° C., although other fusible salt mixtures have been used, such as alkali metal thiocyanates, as well as solid electrolytes, such as the alkali metal aluminum chlorides. Suitable active cathode materials that are reduced in the electrochemical cell reaction include phosphates, metal oxides, borates and chromates. The terms cathode, depolarizer and depolarized cathode are frequently used in discussions of battery technology. Herinafter, only the term "cathode" will be used, and will be understood to embrace the meanings carried by any of these terms.

Lithium is an attractive anode because of its reactivity, light weight and high voltage (between 1.6 and 3.6 volts, depending on the cathode material). The advantages of lithium include high energy density, flat discharge characteristics, and good shelf life.

Known thermal batteries usually employ the following cell construction (although other cell constructions are known). The anode is provided by a layer of lithium either in the form of the pure metal held in a support (since the metal is liquid in the thermally activated state) or in the form of an alloy, e.g., with boron, silicon or aluminum. The electrolyte is a pressed powder pellet comprising a eutectic mixture of LiCl and KCl, or of LiF, LiCl and LiBr. The electrolyte is admixed with an inert binder such as MgO to immobilise it when molten.

Several cells are arranged in a stack, each cell having its own pyrotechnic pellet. The stack is assembled in a dry atmosphere and is enclosed by material providing a thermal blanket. The enclosed stack is then hermetcially sealed within a steel case.

The common cathode materials known to be used in thermal batteries are CaCrO₄, V₂ O₅ and FeS₂. Of these, CaCrO₄ and V₂ O₅ are soluble in molten LiCl/KCl eutectic. Therefore, a portion of the active cathode material must be expended in the formation of a separator layer to prevent self discharge. Cathodes of these materials are also subject to concentration polarization in the course of discharge.

FeS₂ is insoluble in the LiCl/KCl eutectic, hence avoiding the two difficulties mentioned above. FeS₂, however, possesses limited thermal stability, undergoing thermal decomposition in LiCl-KCl eutectic at about 550° C.

Conventional room or ambient temperature cells having lithium anodes are also known. Such cells have the advantages given previously.

Nonaqueous solvents are used as the electrolyte because of the solubility of lithium in aqueous solutions. Organic solvents, such as acetonitrile and propylene carbonate, and inorganic solvents, such as thionyl chloride, sulfuryl chloride and sulfur dioxide, are typical. A compatible solute is added to provide the necessary electrolyte conductivity. A number of different materials, e.g., sulfur dioxide, carbon monofluoride, vanadium pentoxide, manganese dioxide, copper sulfide, and the like, have been used as the active cathode material.

It is therefore an object of the present invention to provide a novel cathode material for thermal cells.

It is another object of the present invention to provide a novel cathode material for conventional lithium cells.

Other objects, aspects and advantages of the present invention will become apparent to those skilled in the art from a reading of the following detailed description of the invention.

SUMMARY OF THE INVENTION

In accordance with the present invention, there is provided a primary cell having an anode material, an electrolyte material and a cathode material, wherein the cathode material, in the pre-discharge condition thereof, is Na₆ V₁₀ O₂₈.

In one aspect, the invention comprises a thermal cell having a lithium metal or lithium alloy anode, an electrolyte material comprising at least one lithium salt and the aforementioned cathode material.

In another aspect, the invention comprises an improved conventional room or ambient temperature cell having a lithium anode, a nonaqueous electrolyte and the aforementioned cathode material.

In the thermal cell, the anode may be a known lithium based anode, e.g., comprising pure lithium held in a known container or support, or comprising a suitable known lithium alloy, e.g., containing one or more of boron, silicon or aluminum.

The anode material may optionally be mixed with electrolyte or contacted by electrolyte contained in a pad. The content of lithium in the anode material, excluding any electrolyte present, is generally about 5 to 85 weight percent, depending on the manner in which the lithium is contained.

If the lithium is contained in an unalloyed state, it preferably forms about 5 to 30% of the overall weight of lithium plus support material in which it is contained. Such support material may be an inert matrix, such as an iron mesh or a porous nickel/chromium matrix. Typically, the lithium forms 7 to 8% by weight of such anode materials.

If the lithium in the anode material is provided in the form of an alloy, it is preferably selected from (1) lithium-aluminum alloys containing about 20 to 50 weight percent lithium, balance aluminum, (2) lithium-silicon alloys containing about 44 to 56 weight percent lithium, balance silicon, and (3) lithium-boron alloys containing about 53 to 80 weight percent lithium, balance boron.

Suitable electrolytes include the solid electrolytes, such as the alkali metal aluminum chlorides, and liquid electrolytes. The liquid electrolyte should have a melting point less than 650° C., preferably about 300° to 500° C. Suitable liquid electrolytes include LiCl/KCl eutectic (m.p. 364° C.), LiF/LiCl/LiBr eutectic (m.p. 450° C.), and LiBr/KBr

In the room temperature cell, the anode is generally lithium foil. The electrolyte is a nonaqueous solvent, such as acetonitrile or propylene carbonate, saturated with a lithium salt, such as LiBr or LiAsF₆.

In both the thermal cell and the room temperature cell, the cathode is made of finely divided Na₆ V₁₀ O₂₈. The Na₆ V₁₀ O₂₈ as described in Example I, below. In the thermal cell, the cathode material is admixed with electrolyte material prior to pressing the cathode into its disk or pellet form.

In both the thermal cell and the room temperature cell, the selection of the electrolyte and the anode, as well as cell construction, is conventional as will be obvious to those skilled in the art.

The following examples illustrate the invention:

EXAMPLE I Preparation of Na₆ V₁₀ O₂₈

Sodium vanadate (50 g) was dissolved in 900 ml of water, then filtered. To the filtered solution, 250 ml of a NaOAc/HOAc buffer solution (ph 5) was added. About 300 ml of 95% ethanol was added to the buffered solution. The resulting solution was cooled for several hours. Yellow-orange crystals of Na₆ V₁₀ O₂₈ ×2H₂ O were filtered, washed with a small amount of 95% ethanol and dried in air. The crystals were further dried in vacuo at 80° C. for several hours. Analysis calculated for Na₆ V₁₀ O₂₈ ×2H₂ O: V, 45.03; H₂ O, 3.18. Found: V, 45.27; H₂ O, 3.0. The DSC of this material did not display any significant exothermic process in the 50°-500° C. range.

EXAMPLE II

Cells were constructed using a 1.5 g 28 wt. % LiAl anode, 3 g of LiCl/KCl eutectic with a binder as the electrolyte and a 3 g pellet of Na₆ V₁₀ O₂₈, admixed 1:1 with electrolyte material, as the cathode. The cells were heated to the temperatures (° C.) shown in Table I, below, under argon, and discharged through a constant current load, expressed in amps. In the Table, the term Current is expressed in amperes, Vp means peak voltage, expressed in volts, tn means the active life of the cell from initiation to n% of Vp, expressed in seconds, and EDn means energy density of the cell over the period tn, expressed in watt-hr/kg.

For comparison, cells comprising known cathode materials were also constructed and tested. Their data are given in Table II, wherein the header units have the same meaning as in Table I.

                                      TABLE I                                      __________________________________________________________________________     Cathode                                                                               Temp                                                                               Current                                                                             Vp t90                                                                               t80                                                                               t70 ED90                                                                               ED80                                                                               ED70                                      __________________________________________________________________________     Na.sub.6 V.sub.10 O.sub.28                                                            400 0.93 2.43                                                                              413                                                                               729                                                                               828 32.7                                                                               55.2                                                                               61.4                                             425 0.93 2.51                                                                              414                                                                               947                                                                               1111                                                                               33.9                                                                               76.1                                                                               86.7                                             450 0.93 2.59                                                                              284                                                                               695                                                                               931 24.0                                                                               55.2                                                                               71.0                                             475 0.93 2.81                                                                              129                                                                               354                                                                               596 11.6                                                                               30.1                                                                               47.7                                             500 0.93 2.88                                                                              139                                                                               307                                                                               423 11.0                                                                               25.1                                                                               34.0                                             525 0.93 2.71                                                                               73                                                                               231                                                                               346  6.7                                                                               19.9                                                                               28.5                                      __________________________________________________________________________

                                      TABLE II                                     __________________________________________________________________________     Cathode                                                                              Temp                                                                               Current                                                                             Vp t90 t80 t70                                                                               ED90                                                                               ED80                                                                               ED70                                      __________________________________________________________________________     FeS.sub.2                                                                            450 1.0  2.10                                                                              1072                                                                               2330   67.6                                                                               139                                                 450 1.0  2.06                                                                              1143                                                                               2150   79.7                                                                               142                                           V.sub.2 O.sub.5                                                                      400 0.993                                                                               3.23                                                                              142 182 518                                                                               16.0                                                                               19.5                                                                               52.3                                            425 0.995                                                                               3.26                                                                              145 201 404                                                                               16.5                                                                               21.7                                                                               41.3                                            450 0.992                                                                               3.28                                                                              105 130 294                                                                               12.3                                                                               14.1                                                                               30.1                                            475 0.993                                                                               3.28                                                                               84 209 310                                                                               9.63                                                                               22.7                                                                               31.8                                      MoO.sub.3                                                                            400 0.987                                                                               3.01                                                                              220 300 375                                                                               23.0                                                                               29.7                                                                               35.1                                            425 0.985                                                                               3.05                                                                              225 289 302                                                                               23.8                                                                               28.9                                                                               29.0                                            450 0.990                                                                               3.04                                                                              183 230 245                                                                               20.4                                                                               23.1                                                                               23.2                                            475 0.987                                                                               3.02                                                                              141 165 179                                                                               14.8                                                                               16.4                                                                               16.8                                      Nb.sub.2 O.sub.5                                                                     400 0.985                                                                               2.03                                                                               74 253 447                                                                               5.2 16.9                                                                               28.1                                            425 0.982                                                                               2.06                                                                               67 232 452                                                                               4.77                                                                               15.6                                                                               28.8                                            450 0.988                                                                               2.07                                                                               79 208 396                                                                               5.59                                                                               14.0                                                                               25.1                                            475 0.985                                                                               2.12                                                                               60 187 399                                                                               4.40                                                                               13.0                                                                               26.2                                      __________________________________________________________________________

Examination of the data reveals that in comparison to FeS₂, the cathode material of this invention provides higher cell voltage. When compared to the other cathode materials in Table II, the lifetimes, energy densities and discharge profiles of the cathode material of this invention are superior to known cathode materials.

The cathode material of this invention is a polyanion. The polyanion is somewhat polymerized, thus being more massive than the simpler materials listed in Table II. Because of its size, the cathode material of this invention has little tendency to dissolve in the molten salt electrolyte and diffuse or migrate across the cell to the anode site. While massive, the material has a large electrochemical equivalence.

Various modifications may be made to the invention as described without departing from the spirit of the invention or the scope of the appended claims. 

I claim:
 1. A primary cell having an anode material, an electrolyte material and a cathode material, wherein said cathode material, in the pre-discharge condition thereof, is Na₆ V₁₀ O₂₈.
 2. A thermal cell in accordance with claim 1 wherein said anode material is lithium metal or any alloy of lithium.
 3. The cell of claim 2 wherein said cathode material is in intimate admixture with an electrolyte material comprising at least one lithium salt.
 4. The cell of claim 3 wherein said electrolyte material is LiCl/KCl eutectic.
 5. The cell of claim 3 wherein said electrolyte material is LiF/LiCl/LiBr eutectic.
 6. The cell of claim 3 wherein said electrolyte material is LiBr/KBr eutectic.
 7. The cell of claim 2 wherein said anode material is a lithium/aluminum alloy containing about 20 to 24 weight percent lithium.
 8. The cell of claim 2 wherein said anode material is a lithium/silicon alloy containing about 44 to 56 weight percent lithium.
 9. The cell of claim 2 wherein said anode material is a lithium/boron alloy containing about 53 to 80 weight percent lithium.
 10. A primary cell in accordance with claim 1 wherein said anode material is lithium metal and wherein said electrolyte material is a nonaqueous solvent.
 11. The cell of claim 10 wherein said electrolyte material is an organic solvent.
 12. The cell of claim 11 wherein said electrolyte material is acetonitrile.
 13. The cell of claim 11 wherein said electrolyte material is propylene carbonate. 